HomeMy WebLinkAboutcut sheetsBOARD OF
COUNTY
COMMISSIONERS
ST.
COUNTY
Lure!
E
F L
O R
I D
A
GAS PIPING SCHEMATIC
[A2]
[L4]
TANK L1 L3 LS
SIZE
L2] l[L6]
[A1] [A3]
TANK SIZE: 250 GALS.
APPLICANCE — TYPE/SIZE
Al Generator
A2
A3
A4
A5
A6
PIPING LENGTH & SIZE
[A4]
[L8]
L7 L9] [L11
[L10]
[AS]
400,000 BTU
BTU
BTU
BTU
BTU
BTU
L115
FT.
3/4 INCH DIA.
L21
FT.
3/4 INCH DIA.
L3
FT.
INCH DIA.
L4
FT.
INCH DIA.
L5
FT.
INCH DIA.
L6
FT.
INCH DIA.
L7
FT.
INCH DIA.
L8
FT.
INCH DIA.
L9
FT.
INCH DIA.
L10
FT.
INCH DIA.
L11
FT.
INCH DIA.
L12
FT.
INCH DIA.
PLANNING & DEVELOPMENT
SERVICES DEPARTMENT
Building and Code Regulation
Division
[A6]
[L12
(PIPE SIZE WAS TAKEN FROM
THE 2014 FBC FUEL GAS CODE —
TABLE 402 ( ))
Website: www.stlucieco aov
2300 Virginia Avenue - Fort Pierce, FL. 34982-5652
Phone (772) 462-1553 FAX (772) 462-1578
Revised 7/22/14
120-2,000 wg
Finished with ArcClad'
Superior Aboveground Coating
8" dome in black plastic or galvanized steel
01'.IPIANII4i��TC1
A*
S Tank Fea
ures:
• Dual service
options for above or under
ground 13pplications
Option 1
Superior, ready to bury, red
oxide dL
rable powder coating with black
polyeth
len dome'
Option
: Aboveground option with
ArcClacl
coating and an 8" steel
AGUG d
me
•. a ncated to A.S.M.E. code, Section VIII, Division 1 •
All valve and float gauge are centered
= =W' Registered with the National Board
under dc me
For more €n,ormaCio-r,'
#Vacuuni Purged
888.558.8265 #72 liqui level outage valve orifice
0
D
w
S
0
c
0
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GENERAL SPECIFICATIONS
Conforms to the latest edition and addenda of the ASME code for
Pressure Vessels, Section Vill, Division 1. Complies with NFPA 58.
Rated at 250 psig from -202 F. to 1251 F. All tanks may be
evacuated to a full (14.7 psi) vacuum.
Vessel Finish: Coated with epoxy and red powder. (Tanks coated
with the epoxy powder must be buried). For Aboveground use,
tanks will be coated with ArcClad; zinc rich epoxy primer and
super durable TGIC polyester topcoat.
'Applicable federal, state, or local regulations may contain specific requirements for protective co,
installer are responsible for compliance with all federal state, local and NFPA Industry regulations.
continuous and uninterrupted and must comply with local, state or national code.
Water Ouislde Head Overall Overall Leg
Capacity Dlameter Type Length Height Width
120 wg• 24" Ellip 5' - 513/16" 3' - 3/16" 101/8"
454.21- 609.6 mm 1.671.6 mm 919.1 mm 2572 mm
250 wg• 31.5" Hemi T - 21/2" 3' - 711/16, 12 3/4"
946.3 L 800.1 mm 2,1971 mm 1.109.6 mm 323.9 mm
320 wg. 31.5" Hemi 8'-113/4- 3' - 711/161 12 3/4"
1,211.2 L 800.1 mm 2.736.9 mm 1.109.6 mm 323.9 mm
500 wg. 37.42" Hemi 9' -10" 4' -15/8" 15"
1,892.5 L 950.5 mm 2,997.2 mm 1,260.4 mm 381,0 mm
1000 wg. 40.96" Hemi 151-1013/16"
3,785.0 L 1,040.4 mm 4,846.E mrn 1,350.9 mm 412.8 mm
All vessels dimensions are approximate.
Fog' More infol'marl01 J
888.558.8265
OVERALLLENGTH
DOME
I I
I I
I I
I I
I I
I
P
I I
LEG SPACING
WITHDRAWAL
�--�� VALVE
ANODE
CONNECTIO14
oO M ', FILLER
I ^ � VALVE
r ` O
YE NAME
_-,�- PLATE
EUEF
and cathodic protection. The purchaser and
dic protection is required and coating must be
Leg
uuallty
Spacing
Weight
Full
Per
Load
Stack
245 lbs.
96
12
914.4 mm
1111 kg.
3' - 6"
472 lbs.
63
9
1,066.8 rnm
2143 kg.
4' - 01/4"
588 lbs.
45
9
1.225.6 mm
266.7 kg.
5' - 0"
871 lbs.
30
6
1.524.0 mm
3953 kg
9' - 0"
1,729 lbs
15
5
2,743.2 mm
784.3 kg.
Eng. Update: April 5.2()16
Why Tanks Corrode
Underground steel tanks corrode due to an electrochemical reaction
between the tank and the surrounding soil. The process of corrosion
occurs due to small voltage differences on the steel surface that result
in the flow of DC current from one location to another. Where current
flows from the tank into the soil corrosion occurs. This location is called
the anode in a corrosion circuit. Where currentflows from the soil to the
tank, no corrosion occurs. The progress of corrosion is determined by
the amount of current flowing between the anode and -the cathode and
whether the locations of the anode/ cathode remain constant over time.
Corrosion rates are generally higher in wet soil environments since the
conductivity of the soil promotes the flow of DC current in the corrosion
circuit.
Corrosion generally exhibits itself on underground tanks in either a
general overall rusting or more commonly, a pitting attack Pit locations
may result from metallurgical conditions of the steel surface or soil
variations such as rocks, salts, fertilizer, moisture concentration, oxygen
concentration, etc.
Preventing Corrosion
Protecting underground
tanks from corrosion is
easily achieved by the use
of two commonly applied
protection methods:
external coating and
cathodic protection.
These two methods
are complementary
and should be used in
conjunction with the
other. An effective
eernal protective
coating insulates the steel from the soil envinr nt, thus preventing
the flow of corrosion current from the anode to the cathode. An effective
external coating can protect over99% of the tank surface area. However,
no coating is perfect. Damage from construction or soil stresses create
tiny defects, which may result in accelerated corrosion at the defect.
Cathodic protection prevents corrosion at those defects by applying
DC current from an external source, forcing the tank to become
cathode. Application of sufficient DC current to the tank will prevent any
corrosion from occurring. The two general types of cathodic protection
systems are sacrificial and impressed current. Sacrificial systems are
used when the amount of current required for the protection is small,
such as in underground propane tanks. Impressed current systems
are more commonly used for large structures such as large diameter
pipelines. Electrical isolation of the tank from metallic piping systems
and -electrical grounds- is -critical for the cathodic protection-syst:em's,
effectiveness.
How Sacrificial Cathodic Protection Works
Sacrificial systems work by creating a galvanic connection between two
different metals The most common anode material is magnesium,
which when c -pled to steel results in DC current flow from the
magnesium to he steel. The open circuit potential of steel is about
-0.50 volts refei nced to a copper sulfate electrode. The open circuit
potential of mac nesium is about -1.55V to-1.80V. By connecting the
two metals togs er, the difference of 1 to 1.25V volts results in current
flow to the tank hat overcomes the natural corrosion cells that exist on
the tank With is current available to the tank, no corrosion occurs.
Magnesium Anc des
There are a va 'ety of anode sizes and alloys used for cathodic
protection. The wo primary alloys are designed as H-1 (or AZ63) and
High Potential. a H-1 alloy is produced from recycled magnesium
and has an open circuit potential of approximately—1.55V. This alloy
Is well suited for protection of underground propane tanks. The High
Potential alloy is 9% pure magnesium having an open circuit potential
up to -1.8V. This alloy should be used for soil applications over 10,000
ohm -cm resisfMlv
The two most c mmon anode sizes used for underground propane
tanks are 9 lb. an 171b. The size designation relates to the metal weight.
10' of #12 TW i sulated wire is attached to the anodes. Anodes are
then backfilled in a mixture of gypsum, bentonite, and sodium sulfate
to lower the elect cal resistance of the anode to soil. The mixture is a
low cost, north does, electrically conductive backfill. The anode and
backfill is then pa kaged in a cotton bag and either a cardboard box or
paper bag. Actua I shipping weight of these anodes with backfill is 27
lb. and 45 lb.
Application Reco mendations
Magnesium ano can protect underground tanks in most soil
conditions. The H 1 alloy is generally very effective. The following chart
provides size and c jantity recommendations for various size tanks based
on conservative dt sign assumptions. This chart covers soil conditions
UP to 10,000 oh -centimeter resistivity. Resistivities higher than
10,000 ohm -centimeter generally represent very dry soils. Verification
of soil resistivity can be performed through soil analysis. Contact us
for design recomrr endations in locations where soil resistivities exceed
10,000 ohm -cm, o if there is no effective external coating on the tank.
The propane servi a line from the tank to the house also must be
considered in the athodic protection design, unless the service line
is plastic. All and ground steel pipe should be externally coated with
a corrosion resists t material. The service line should be electrically
isolated at the hou a with an insulating fitting or union. If service pipe
is less than 50' in It ngth, the tank anodes will provide sufficient current
to protect both taril and pipe. For longer lengths of pipe, an additional
anode may be requ red at the house connections.
If another- metallic Material such as copper -is 'Used for service piping- - - - - - -
the pipe should be electrically isolated from the tank at the fill pipe
connection. Copper and steel create a galvanic couple that will accelerate
corrosion of the steel tank when directly connected to copper piping.
Generally, copper piping does not require cathodic protection.
Soil Type
Fertile Sails, Clay,
Sand, Gravel, Rocky
Sandy Loam
Areas
Tank Cap.
5 to 50H ohm -cm
5000 to 10009 ohm -cm
(gal.)
Size Oty. Alloy
Size
Qty.
Alloy
120
W 1 H-1
91
1
H-1
150
W 1 H-1
9#
1
H-1
250
9# 1 H-1
91
2
H-1
325
9# 1 H-1
9#
2
H-1
500
17# 1 H-1
9#
2
H-1
1000
17# 2 H-1
91
4
H-1
1500
17# 2 H-1
9#
4
H-1
2000
170 3 H-1
9#
li
H-1
'Based on 90% effecdve external coating, 2 ma/ft2 current density, and 30-
ye2rAnode life.
Anode Installation
1. Determine size and quantity of anodes from application chart.
2. When a single anode is installed, it should be located near the
tank center on either side of tank.
3. When multiple anodes are installed, space them evenly around
the tank. See examples below.
1 anode �2 anodes 4 anodes
fi�`^m
`�- _ .. _
4.Anodes are shipped in either cardboard boxes or multi -wall
paper sacks. Remove outer container and burythe cloth bagged
anode. If anode is supplied in plastic bag, remove plastic bag
before Installing.
5. Install anodes approximately two to three feet from the tank and
at least as deep as the center line of the tank. Anodes work best
in locations with permanent moisture, so generally the deeper
the better.
6. After placing the anode, stretch out the anode connection wire
and extend over to a connection point on the tank fill pipe.
7. Cover the anode with approximately six inches of backfill and
pour 5 gallons of water on the anode to saturate the prepared
backfill. Water is necessary to activate the anode.
8. Connect the anode wire to the tank with a low electrical
resistance connection. Examples are threaded stud on the
tank fill pipe or any accessible metallic connection point to the
tank. All connections should be coated with a moisture -proof
material.
9. Ideally, the tank connection is made in the area of the tank fill
Pipe within the covered dome. With access to the anode wire,
subsequent testing of the tank can include measurement of
anode output and verification of performance.
10.Verify performance of the anode using an appropriate test
procedure.
ica► Connection Under Dome
r
2'41
ratnpdic Protection Testing Procedure
Equipment Nee ed: Digital Voltmeter, Red Test Lead Min. 12' Long
& Black Lead Alin. 2' Long, Reference Electrode (Copper/Copper
Sulphate Half -Cell)
STEP 1: Using a igital voltmeter insert the red test lead into the Volt
jack of the mete and select the 2 or 20 volt DC scale. Clip red test
lead connector t an uncoated metallic area of the tank, preferably
to the fill pipe mi Itivalve. A good solid connection is very important.
(DO NOT conne(t to shroud).
STEP 2: Insertth blacktest lead into the Common jack on the meter,
and connect the opposite end of the lead to a charged reference
electrode ('ri cell .
STEP 3: Remove protective cap from the porous plug at bottom end
of electrode. Pla a porous plug end into native soil (remove grass if
necessary) at foL r locations around the tank (one on each side of the
tank, and one at each end of the tank). If difficulty is encountered
obtaining readin s, moisten soil with water or dig Yz cell deeper into
the soil.
STEP 4: Record II four meter readings on an appropriate form. The
least of all four r adings should be a minimum of-0.850v or more
negative. {Note: any of the four readings are below (less negative)
-0.850v then the ank is not fully protected).
Charging Reference Electrode
STEP 1: Unscrew and remove porous plug and of new reference
electrode. Add eionized or distilled water to the copper sulfate
crystals, filling el ctrode completely. The solution will turn blue in
color and there s lould always be excess crystals at the bottom of
the tube. DO NO USE TAP WATER.
STEP 2: Replace I Drous plug end of electrode and place in an upright
Position so that t e porous plug end is facing in the down position
and let stand for hour before use. This will allow the porous plug
to become compl tely saturated before use.
Caution: Do not a tow electrode to contact oil, road salts, or other
substances that may contaminate the solution by absorption
through porous p g. Do not allow electrode to freeze.
! Distributed By:
1 moI i-sooe
ES-D-GAC—Generator Generac
Job Name _
Job Location
Engineer _
Approval
Contractor
Approval _
SKU
Dor nont Supr-Safe®
Flexible Gas Appliance
Connectors
The flexible connection between the gas supply and the gas Inlet
of a Generac• Stationary Outdoor Backup/Standby Generator.
Features
• Operating Temperature -40•F to 1501F (-401C to 65.6'G7
• Operating Pressure MAX 0.5psi (3.45 kPa)
• Hydrostatic Burst Pressure MIN 250psi (1725 kPa)
• Fle:abie Tube Material Annealed 304 Stainless Steel
• Flare Nut Material Carbon Steel with Zinc Trivalent
Chromate Plating
• Flare Adapter Material Carbon Steel with Zinc Trivalent
Chromate Plating
CSA Group Certificate of Compliance to
Product Standards
ANSI Z21.75/CSA 6.27 — Connectors for Outdoor Gas Appliances
and Manufactured Homes
Scope states '...intended for exterior use above ground for making
non -rigid connections... between the gas supply and the gas inlet
of an appiiance for outdoor installation that is not frequently moved
after Installation.' In addition section 1.5.4 states the connector Is
designed for occasional movement after installation. Repeated bend-
ing, flexing or extreme vibration must be avoided. Normal opera-
tion of a clothes dryer, rooftop HVAC unit or SIMILAR OUTDOOR
APPLIANCE DOES NOT constitute extreme vibration or movement.
ANSI Z21.24/CSA 6.10 — Connectors for Gas Appliances
(Excluding 60/51 Series)
CIF us
Product Configurations
both English and rtancn
" r
Alf installations must completely comply with all Domwnt manufacturing company warnings
and Instructions, national, state and local codes and all applicable ansi standards.
Applicable
ANSI Z223.1/NF
International Fue
8149.1 — Natura
(CSA C
Uniform Mechan
Uniform Plumbin
No.
For use with Generac
stationary outdoor backup/
standby generators.
Series 30, 40 and 60
'A 54 National Fuel Gas Code Section 9.6
Gas Code (IFGC) Section 411.1
Gas and Propane Installation Code
'oUp) Section 621
rat Code (UMC) Section 1313.0
Code (UPC) Section 1212.0
Additional pprovais
Commonwealth f Massachusetts Board of State Examiners
of Plumbers and 3aa Fitters
Additional sting
UL2200-2015: S Uonary Engine Generator Assemblies
Section 66B Vtbr Test.
Doman[ Product specircadons in U.S' customary units and metric are approodnraie and are provided for reference only. For precise
MM please eoehut DormontTechnical Service. Dormant resenys the right to change or modify pnxW dosrfln, conspucUon, SM
or materials without prior notice and without h uoing any obligation to make such charges and modfce lane an llormpd product
or subsequently sold. Rehr to the oymers manual for warranty krforrnaton
rR
... - DSrmonr
A WAFTS Brand
Minimum Flow Capacity at Specified Pressure
Drop
(Straight Length BTU/hr. NATURAL GAS, 0.64 SG, 1000 BTU/cu.ft.)
CXIFIGURATION
Generac Part Number DMWt Part Nambdr SFAIES Nominal ID
NOIT" Langth
I
OL4835A CAN30-3131-14GL 30 r/:
m
14
OL4836A CAN40-4141-14GL 40
14
OL4938C CAN60-6161-15GL 60 1-/
15
(Straight Length BTU/hr. LP GAS, 1.55 SG, 2500 BTU/cu.fL)
Gen= Part Number
Dormont PaA Number SERIES
Nominal lo
Nominal Length
OL4835A
CAN30 3131-14G1 30
%
to
14
OL4636A
CAN40-4141-14131. 40
%
14
OL4836C
CAN60-6161-15GL 60
1-1/,
11: ,
Dormont part number CM30-3131-140L can supply a minimum of 349,000 BTU/hr,
of natural gas a 2 0o in. water column pressure drop to the generator.
D6(Mon �®......
.....
A VAM Brand
ES-D-GAC_Gener8tor Generac 1651
0.50 !n
a75 in01,6M56,500
7.25 in 7.50/n
1.756
200 in
174,500
213,500
275,500 302.000
326,000
349,00(
338,500
414,500
535,0D0 586,000
633,000
677,00(
,171,500
1,434,500
1,852.000 2.029AM
? 1Q1 nnn
I'TeI M
kr 11 ?S 61 I 1.50b7 1.751n I 200 M
uu 1 44Q800 1483,200 1 521.600 riSa e(v
USA: Tel: 000) 367-6668 • Fax (7-74) 733-4808 . Donnont.corn
Canada : (96o) 332-4pe0 - Fax: (e05) 332-7068 - Dormont.ca
Latin America; Tek (52) 81 1001-woo - Fax: (52) 81-8000-7091 • Domtont.com
0 2016 Dorrnont
Ideal for use as a first stags regulator on any domestic silo ASIIAE or
DOT container in propane gas installations requiring up to 1,500,000
BTU's per hour. The regulator is factory set to reduce container UL
pressure to an intermediate pressure of approximately 10 PSIG.
LV3403TR "
LV3403TRV9 Y4" F. T/2" F.NPT r/ai' 10 PSIG 7"h7-�
rdexlmum 'low based on inlet Pressure 20 PSIG higher tan the regulator sethe regulator selling end delivery pressure 20% lower than the setting. and delivery pressure
Provides accurate first stage regulation In two -stage bulk tank
to
systems. Reduce tank pressure to an intermediate pressure of to 10 IN
PSIG. Also used to supply high pressure burners for applications like �L
Industrial furnaces or boilers. Also Incorporated In multiple cylinder
Installations.
L114403SR4 I W FINTIMMM
LV4403TR4 I NPT ,, F
10 1-5
LV4403SR9 NPT
5-10
LV4403TR9
F. POL
'/+" 5 1-5
10 Yes
5 10
2,500,000
LV-403SR90
I.V4403TR96 N
F NPT
10 5-10
' When used for finalilstage pressure control, must either Incorporate integral roller valve or sopruato rdbr valve should !>e
with NFPA Pam
" Maximum lbw based on inlet Pressure 20 PSIG
higher then the regu(ator setting and delivery
Good In accordance
Pressure 20% lower uran
setdng.
Designed to reduce first stage pressure of 5 to 20 PSIG down to
burner pressure, normally 11" w.c. Ideal for medium commercial
installations, multiple cylinder installations and normal domestic 0loads.
LV440384 �= r "
LV4403846 W F. NPT
LV4403848R' #28 11" w.c. at 9' to 13'
'/1 F. NPT Drill 10 PSIG w.c. Over Inlet 35,000 LV44038i36 Inlet
LV440336611• %" F. NPT
aaekmeunt design
Maximum Dow based on 10 PSIG inlet and 9 :w.o. delivery pressure. -
9.V3403TR
Mw3 series
ILV4403Rseries
r,
100 Rego Dr. Elul.. NC 27244 USA vnvw.. o ` —? r ;+•r" "--'•
'Cg products.corn +1 (330) 4a9-7707
3 12
U U IV
wlevouound Gas � � �� 'C.9 � �� L3 .rY' Piping
Fitting Assembly & SUing COog,
IT
b
STC-P 't
Verity the polyethylene
(P E.) pipe being
assembled is the
correct size.
SJP 2
Cut pipe ends square.
STEP
Clean Piping thoroughly
to assure there is no
dirt grease or oil in
assembly area.
STEP 4
Chamfer end of pipe
using Continental's
chamfering tool with I.D.
gouge.
ID of PIPE
Patent #s 5.366,260,5,692,785 & 5,853,272
Ph: 1.800.662.0208 o Fax: 615.325.9407 " Web: www.gastite.com
syiip 8
Mark the stab depth by
inserting the pipe into
the chamfer tool and
marking the pipe at the
entrance as shown.
a'e'CP G
If using chamfer tool
with 11) gouge, check
for proper chamfer by
f Inserting pipe over
gauge.
STEP 7
Stab pipe completely
�--• Into fitting entrance.
4 STEP 8
Stab pipe completely
into filling so that the
mark on the pipe is
within 1/8" from the
fitting entrance.
STEP 9
Repeat steps 1 though 4 for all Con -Stab joints.
SUP 10
To assure prop r assembly and to comply with 49
CFR 192 Subp It J-Test requirements, the joint shall
be teak tested.
a
Maximum Copaclty of PE Pipe In Thousands of BTUg�per H r of Uquefted Petroleum Gas
With a Gas Pressure of 71.0 In. WC and a Pressur Drop of 0:5 in. WC
(based on a 1,52 specific grow gas
1073
1391
720
934
571
484
425
383
21-4
325
50
45
1983
1331
740
1054
627
893
861
370
3257
33
333
3563
4724
2391
3247
1894
1605
1412
708
12072
6()
10078
528
948
475
854
1.0063
6755
2608
5357
2232
4535
1978
1792
1534
1359
1232
3989
3592
30A4
2679
2411
129
167
a
113
147
18
102
132
15 —13-- 12
86 ..
11 70
76 68 b3 58
► n
9
54
238
427
209
376
188
338
75
160 140 126 7816 107
287 252
70
100
642
1207
569
1061
576
966
227 208
441 192
391
810 391 354 326 303
180
285
642 587 544
508
Maximum Capacity of PC Pipe In Thousands of BTU per Ho
with a Gas Pressure of 2.0
psi and a Pressure
(based on a 1.52 specific gravity gas)
IYoo
11300
1319
7686
]045
886
779
r
°
471
14652
9835
6008
7790
5092
6602
4479
=7
403
341g
3007
20877
14014
11100
9408
8275
5229
7461
�5
3898
32707
510
3510
37514
25183
19946
16905
14869
13389
11348
9982
8
105963
0596
71131
71131
56339
56339
20515
47750
18]82
16474
14100
12496
988
11322
42000
31820
32054
28194
25388
235
218
204
192
169
152
1197
435
403
376
354
31
280
781
723
676
636
560
504
1133
1054
989
934
828
750
2207
20"
1910
1797
1581
1424
66 b3
46
60
44
57
42
40
94
169 160
152
146
54
140
52
269 255
478 453
244
431
233
411
224
134
216
394
379
of Uquefied Petroleum Gas 516BTUh-1CFH
lop of 1.0 psi
76 2295
13
2144
2018
1775
1599
2975
78 4239
2780
3962
2617
2302
2073
t6 7618
7119
3729
6700
3280
5894
2953
5307
17 9691
9092
8589
7612
6897
34 21517
20108
18926
16647
14990
1355
1192
1073
190
910
139
800
125
------�.
1I5
-
106 99
• • r ° ++ ° r -- r-----•..�
93
1757
1545
1545
1391
1179
720
659
611 571
792
37 508
48Q
80 77 74
469 Q74 425
AMEM2503
4498
3956
1983
3563
1880
3019
108
1334
12 g
1128 17054
96 659
627
599 574 551
5903
12705
5232
4740
4057
2666
3596
2391
3258
2189
2-997
2027 1894
2788
1783 169
1893
853 818 786
1144 146)
11175
10063
8529
7602
6755
6182
2616
5725 5350
71 2347
2239
2744 2060 1985
1985
Maximum Capacity of PE Pipe
4767
4535
433) 4150 3988
in Thousands
with a Gas Pressure of
of BTU per Hour
10.0
f Liquefied Pelroleum Gas5168Tuh=1CFH
psi and a Pressure Dr
(based on a 1.52 specific
p of 1.0 psi
gravity gas)
2476
14234
t
1662
9555
7316
7568
1116
6414
981
r
884
°
749
- •
6 •°
593
r '+
3
-
ss r
18455
723"
9812
8316
5642
7315
5080
3787 3410 3121
503
2890
470
442 389.350
26296
17652
13981
17849
10423
6587
9385
583
4997 442
7 3747
2701
3502
2542 2236 2014
47252
53960
31720
37087
25123
21293
18729
16865
7954
14294
5
12572 11321 5,
b340
5340
4990
3296 2899 2611
4697 4131 3720
4131 3720
133416
89601
29782
70967
25489
60148
1
8967
8440 6685
'
529005
477640
40376
35517519 24 31980 29
67 22041
94, 8 8569
°
+ _
re
. _
25�9
20671
70 18882
r 297
261 235
1501
199
or
175
158]707
144 11251146 irt
+ c
r
r,t9i7�`
1946
17531485
100890
1306
769
111
640609
10°6
101
932213
2773
2497
2116�
16
1676
107
15U
932 877862
830
790
557 5363153
7546665 723
7334
4983
650.5890
4487
3803
302, .2757
1421 1328 12
2653.2386
1131125
695
1075 1030 99050414468
14077 12676
10743
9449
4048
-2
3465 3251 307
•26
2916
2022 - .)931-
- -1851• • •177916004
3787
6005
2782
5712
2664 2560 2466
5455 5227 5024
Ph: 1.800.662.0208
a Fax 615.325.9407
a Web:
2b16BTUh=1CFH
www.gastite.com
7